Classifications

• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07H—SUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
  • C07H5/00—Compounds containing saccharide radicals in which the hetero bonds to oxygen have been replaced by the same number of hetero bonds to halogen, nitrogen, sulfur, selenium, or tellurium
  • C07H5/02—Compounds containing saccharide radicals in which the hetero bonds to oxygen have been replaced by the same number of hetero bonds to halogen, nitrogen, sulfur, selenium, or tellurium to halogen
• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07D—HETEROCYCLIC COMPOUNDS
  • C07D407/00—Heterocyclic compounds containing two or more hetero rings, at least one ring having oxygen atoms as the only ring hetero atoms, not provided for by group C07D405/00
  • C07D407/02—Heterocyclic compounds containing two or more hetero rings, at least one ring having oxygen atoms as the only ring hetero atoms, not provided for by group C07D405/00 containing two hetero rings
  • C07D407/12—Heterocyclic compounds containing two or more hetero rings, at least one ring having oxygen atoms as the only ring hetero atoms, not provided for by group C07D405/00 containing two hetero rings linked by a chain containing hetero atoms as chain links
• • C—CHEMISTRY; METALLURGY
  • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
  • C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
  • C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
  • C12N9/10—Transferases (2.)
  • C12N9/1048—Glycosyltransferases (2.4)
  • C12N9/1051—Hexosyltransferases (2.4.1)
• • C—CHEMISTRY; METALLURGY
  • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
  • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
  • C12P19/00—Preparation of compounds containing saccharide radicals
  • C12P19/12—Disaccharides
• • C—CHEMISTRY; METALLURGY
  • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
  • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
  • C12P19/00—Preparation of compounds containing saccharide radicals
  • C12P19/18—Preparation of compounds containing saccharide radicals produced by the action of a glycosyl transferase, e.g. alpha-, beta- or gamma-cyclodextrins
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
  • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10S435/00—Chemistry: molecular biology and microbiology
  • Y10S435/8215—Microorganisms
  • Y10S435/822—Microorganisms using bacteria or actinomycetales
  • Y10S435/832—Bacillus
  • Y10S435/839—Bacillus subtilis

Definitions

• This invention relates to the preparation of fructosyl disaccharides, and especially halosucrose sweeteners, in particular 4,1',6'-trichloro-4,1',6'-trideoxy-ga/actosucrose (known as sucralose), by means of an enzymatic reaction.
• halosucrose sweeteners in particular 4,1',6'-trichloro-4,1',6'-trideoxy-ga/actosucrose (known as sucralose)
• 4,1',6'-trichloro-4,1',6'-trideoxy-ga/actosucrose is a potent sweetener described and claimed with other chlorosucrose derivatives in U.K. Patent No. 1543167.
• Analogues in which the 6-hydroxy group is etherified or missing are disclosed in EP 0103479A and GB 2127806A.
• Analogues containing other halo substituents are disclosed in GB 2104063A.
• One method of preparation of sucralose is described and claimed in GB 2079749A and U.S. 4 380 476.
• This method involves the preparation of a 6-ester of sucrose, or a mixture containing predominantly the 6-ester of sucrose, and then selectively chlorinating this 6- substituted material. Subsequent deesterification at the 6-position yields sucralose. In practice, it is difficult to obtain a sucrose 6-ester in good yield in a specific manner when using chemical means.
• preparation of sucralose from a 6-substituted sucrose derivative can be achieved without difficulty by using an enzyme-based reaction starting from the corresponding 6-substituted glucose and a fructoside sugar, to produce a 6-substituted sucrose free from any other sucrose derivatives substituted at other positions, and easily separable from starting materials and glucose.
• the enzyme in question is a fructosyltransferase.
• Fructosyltransferases are well known in enzymology.
• a representative enzyme is the so-called levansucrase (E.C.2.4.1.10), responsible for the production of levan, a polyfructose derivative, in the decomposition of sucrose or of raffinose.
• levansucrase splits the glucose-fructose link in sucrose and transfers the fructose to an acceptor sugar, e.g. sucrose itself. This process is repeated so that fructose chains are built up. If another sugar is present besides sucrose, e.g.
• the levan formation is inhibited, or at least reduced, and instead the fructose is transferred to the other competing sugar which acts as an acceptor to produce a new fructoside.
• the new fructoside will also act as a donor, so in practice a large excess of donor has been used in order to push the equilibrium in the desired direction.
• Dedonder Methods Enzymol., 8, 500-505 always used a high ratio of fructose donor (e.g. sucrose) to acceptor, e.g. from 5:1 to 10:1, and a low concentration which would not be practicable on an industrial scale.
• a similar reaction is described in U.K. Patent Application 2046757A where a variety of aldose starting materials are reacted with sucrose or raffinose in the presence of a levansucrase derived from a range of microorganisms including Actinomyces viscosus and B. substilis (Strain ATCC 6051, i.e. the Marburg strain).
• the aldose is always an underivatised sugar and the mole ratio of donor to acceptor used is 1:5, presumably in order to minimise chain-forming reactions.
• an enzyme isolated from bacteria which enzyme hydrolyses a donor fructosyl oligosaccharide or disaccharide containing a unsubstituted ⁇ -fructosyI ring attached to the anomeric carbon atom of an aldose by a (1 ⁇ 2) linkage and transfers the fructosyl moiety so released to an acceptor aldose to yield a fructosyl disaccharide as the main product, the enzyme being capable of forming 6-substituted sucrose derivatives as the main product when the acceptor aldose is a 6-substituted glucose, the enzyme producing no significant amounts of alcohol-precipitatable oligo- or polyfructoses in the presence or absence of an aldose acceptor, the enzyme having a K m for sucrose of at least 0.1 M in the absence of an aldose acceptor, the enzyme having a K m for sucrose of at least 0.1 M in the absence of an aldose acceptor
• the fructosyltransferase according to the present invention is preferably derived from B. subtilis or Erwinia sp. (previously known as Aerobacter levanicum).
• B. subtilis is a particularly preferred source because some strains are very easy to grow on a large scale in conventional fermentations and they are well accepted as sources of industrial enzymes (e.g. a-amylases and ⁇ -lactamases).
• the fructosyltransferase is a predominantly exocellular enzyme and can thus be obtained and purified more easily. It is important that the enzyme used should be free of invertase activity. If necessary, a selective invertase-inhibitor must be used, such as p-hydroxymercuribenzoate.
• the Bsubtilis enzyme may be harvested from a B. subtilis liquid culture by selective precipitation or other convenient techniques.
• the culture can be centrifuged to remove cells and debris; brought to about 65% saturation with ammonium sulphate; recentrifuged to remove invertase and other protein contaminants and then brought to about 95% saturation with ammonium sulphate. Crude fructosyl transferase is then precipitated, which can be further purified by being redissolved in phosphate buffer and dialysed.
• the enzyme of choice is the fructosyltransferase obtained from B. subtilis NCIB 11871, although strains NCIB 11872 and 11873 are also of interest.
• the enzyme from these strains also has a broader specificity and can thus be more easily used with a range of 6-substituted derivatives.
• K m The constant K m cited with reference to the enzyme is the Michaelis-menten constant, which is the substrate concentration at which half the maximum rate of enzyme reaction (to produce levan etc) occurs.
• the K m for the strain NCIB 11871 enzyme is abot 0.2M for sucrose in the absence of an acceptor,-while the K m reported for Dedonder's levan sucrase from "B. subtilis BS5", (a clone from B. subtilis var. nigra) was only 0.02M.
• B. subtilis NCIB 11871 and also strains NCIB 11872 and 11873, are typical strains of B. subtilis. That is to say that they meet nearly all the requirements of the species identification, both in classical tests (Berkley and Goodfellow, "The Aerobic Endospore-forming Bacteria; Classification and identification” (1981) Academic Press, London; Gordon, Haynes and Pang, "The Genus Bacilus", Agriculture Handbook No. 427 (1973) U.S. Dept of Agriculture, Washington D.C.) and in the API 50 CHB and API 20E systems (API system S.A. La Balme les Groltes - 38390 Montalieu Vercieu, France and see Logan et al. J. Appl. Bact.
• strain NCIB 11871 is a lactose-negative strain showing variable acid production from xylose.
• Strain NCIB 11872 is lactose negative and also gives negative results with D-mannose, melibiose and trehalose and in the ONPG reaction.
• Strain NCIB 11873 is lactose positive giving negative results with D-mannose and inulin.
• the fructosyltransferases derived from many strains of B. subtilis and Erwinia sp are generally regarded as being levansucrases: that is to say that in the presence of sucrose, they cause the production of levan, a polyfructose material which is alcohol precipitable.
• levansucrases When they are used in the production of fructosyl disaccharides, the competing reaction to produce levan must be suppressed if any useful product is to be obtained, hence the restriction of these enzymes in GB 2046757A to reaction mixtures containing high proportions of the acceptor molecule.
• the B. subtilis NCIB 11871, 11872 and 11873 enzymes used here are much less prone to produce levan.
• the K m for sucrose for 'levan' production is about 0.2 M. This compares with a quoted K m of about 0.02 M for the Dedonder (loc. cit.) BS5 strain enzyme. Even when equivalent concentrations of the acceptor and donor molecules are used and when the conditions are used which were found to promote the synthesis of high molecular weight levan by the Tanaka B. subtilis enzyme (i.e. addition of levan primer, use of a low ionic strength solution, and reaction at low temperatures (J. Biochem 90, 521, 1981)) very little high molecular weight levan is produced. Only after the peak yield of disaccharide is reached is a polymer of intermediate molecular weight formed. Furthermore, unlike other true levansucrases, the enzyme from B.
• subtilis NCIB 11871 appears not to catalyse a disproportionation .reaction i.e. it does not convert low molecular weight oligosaccharides into high molecular weight levan. For instance trisaccharide can be detected, which should not be present if the enzyme carries out the disproportionation reaction.
• Standard levan obtained from Aerobacter levanicum (Sigma) can be fractionated into two peaks corresponding to high and intermediate molecular weight material.
• the Dedonder (loc. cit.) enzyme has an equilibrium constant (levan and glucose/sucrose) of about 3.6 x 10- 2 at 37°C, levan of DP40 being formed.
• strains NCIB 11871, 11872 and 11873 produce an enzyme which produces no significant amount of alcohol- precipitable polysaccharide from sucrose alone, and even the growing cells of strain 11871 produce no levan. It thus appears that the fructosyltransferase produced is not effectively a 'levan sucrase' at all. In this specification it will be referred to as a fructosyltransferase.
• the fructose source for the reaction may be any oligo- or di-saccharide containing a preferably unsubstituted ⁇ -fructosyl ring attached to the anomeric carbon of an aldose by a (1 ⁇ 2) link as in sucrose ( ⁇ -D-fructofuranosyl a-D-glucopyranoside), raffinose (O- ⁇ -D-galactopyranosyl-(1 ⁇ 6 )-0-a-gtucopyranosyi-(1 ⁇ 2)- ⁇ -D-fructofuranoside) or stachyose.
• the 6-substituted aldose starting material of formula II may carry as a protected hydroxy group any substituent of the 6-position which is resistant to the subsequent halogenation reaction and which can be easily removed to release a 6-hydroxy group.
• 6-Carboxylic esters are preferred, e.g., the 6-acetate or benzoate.
• Glucose 6-acetate can be easily prepared by a variety of processes (e.g. Duff, J. Chem. Soc. p 4730-4,1957; Reeve et al J. Amer. Chem. Soc., 79, 4041-3; Frohwein et al Nature p 153, 1960; Duff et al. Nature p 103, 1957; ibid Biochem J. 515-520, 70, 1958).
• the 6-substituent of the aldose starting material of formula II may also be an ether, for example an arylalkyl ether such as the benzyl ether which can be easily removed by hydrogenation or an aliphatic ether which can remain to provide a chlorinated 6-ether as disclosed in GB 2127806A.
• the starting material may also carry, for example, a 4-chloro substituent, to give a disaccharide already partially chlorinated, e.g. 4-chloro-4-deoxy-galactose 6-acetate.
• the reaction between the fructose donor and the fructose acceptor should take place in an aqueous medium, preferably buffered at the optimal pH of the enzyme, i.e. at pH 5.4 ⁇ 6.0 at the optimum temperature of about 30°C.
• the two reactants are generally water soluble and the enzyme may be dispersed in the mutual solution or, preferably, immobilized on an insoluble support. Immobilization may, for example, be effected using an ion exchange resin such as DEAE cellulose, to which the enzyme is strongly adsorbed. Many other immobilizaiton supports may be used, for instance bone char as cisclosed in US 4421850.
• the ratio of fructose donor to fructose acceptor in the reaction mixture is of importance; too low and the yield is reduced; too high and any possible levan reaction may not be suppressed, particularly if a substrate of high solids content is used.
• a molar ratio (donor-acceptor) of about 2:1 is oDtimal.
• the reaction can be effected at fairlv hiah concentration as there is no problem of solubilitv or viscosity.
• a reactant concentration (donor plus acceptor) of about 40% by weight is successful although higher concentrations may be used, depending on the solubility of the reactants, e.g. up to about 75% for glucose 6-acetate.
• the enzyme concentration must naturally depend on the activity, but levels of about 50 mlllitre have been successful when using an aqueous solution containing the enzyme derived from 33 ml of B. subtilis NCIB 11871 clture per ml of solution.
• the subsequent halogenation of a compound of formula III may be effected by use of any reagent capable of displacing hydroxy by halogen selectively in the 4,1'-and 6'-positions.
• a reagent of choice is the Vilsmeier reagent, obtained by reacting a dialkylamide with a chlorinating reagent, e.g. dimethylformamide with phosphorus pentachloride, phosgene or thionyl chloride.
• a chlorinating reagent e.g. dimethylformamide with phosphorus pentachloride, phosgene or thionyl chloride.
• a detailed description of the chlorination of sucrose 6-esters is given in GB 2079749A and US 4 380 476.
• the deprotection of a 6-ester is disclosed in the same publication, using for example sodium methoxide in methanol.
• a 6-benzyl ether group may be removed by hydrogenation.
• the fructose acceptor may, in general be any pyranose or furanose sugar or substituted sugar which it is desired to incorporate in a fructosyl disaccharide.
• examples include 6-substituted glucose derivatives, such as glucose 6-esters and ethers and 6-deoxy-D-glucose, (in the preparation of sucralose and its sweet analogues), or any of the materials suggested for use with a levansucraase in U.K. Patent Application GB 2046757A (but see below).
• the fructosyl di- or oligo-saccharide may comprise sucrose, raffinose, or stachyose.
• sucrose 6-acetate can act as the fructose donor instead of sucrose or faffinose.
• disaccharides including melibiose, lactose, isomaltose, and cellobiose
• disaccharides including lactose, isomaltose, and cellobiose
• certain disaccharides such as lactose and isdomaltulose are unreactive.
• oligosaccharide acceptors are used, the acceptor activity decreases with increasing size, as in the homologous series maltose, maltotriose, maltotetraose etc.
• xylose leading to the production of ⁇ -D-fructofuranosyI (2 ⁇ 1) a-D-xylopyranoside, known as xylsucrose.
• galactose leading to the production of ⁇ -D-fructofuranosyI (2 ⁇ 1 ) a-D-galactopyranoside (galactosucrose).
• Products of this type are low in cariogenicity and/or sweetness, making them of interest as sucrose replacements in areas where excess sweetness is a problem.
• Galactosucrose is interesting particularly because it can be produced from, say, molasses and hydrolysed whey permeate, both readily available sources. It has only a trace of sweetness (ca. 10-15% of sucrose).
• sugars based on sucrose with an a1 ⁇ 2 bond as an absolute requirement are reactive, activity decreasing with the size of the molecule.
• the novel disaccharides formed by the action of the enzyme also act as donors, e.g. xylsucrose.
• the product of the enzyme-catalysed reaction can be separated from the by-products and starting materials by conventional physiochemical means such as chromatography especially high pressure liquid chromatography (HPLC) and ion-exchange resin chromatography.
• HPLC high pressure liquid chromatography
• products having no 6-hydroxy group in the aldose ring for example sucrose 6-esters and ethers, xylose-derived products and 6-deoxy sucrose, have a surprisingly low polarity which makes ion-exchange resin chromatography an easy and effective separation method.
• Polystyrene resins, cross-linked with divinyl benzene, e.g. the Amerblite XAD (regd Trade Mark) resins are particularly suitable. This separation is much easier than the separation of variously substituted sucrose derivatives necessary when the sucrose 6-derivative is prepared by a chemical process.
• the by-product of the fructose transfer reaction using a glucosyl fructoside such as sucrose is glucose itself.
• Glucose is, of course, a potent acceptor, and competes with the desired acceptor, leading to reformation of the starting material. Removal of the glocuse by conversion into fructose can therefore be desirable. This may be achieved by addition of glucose isomerase.
• 6-derivatised sucrose derivatives can be prepared by reacting the corresponding 6-derivatised glucose or galactose with the fructosyl transferase in the presence of sucrose or raffinose or stachyose.
• the product can then be halogenated in the 4,1' and 6'-positions and, if desired, the 6-derivatising group removed to yield the required halosugar.
• the initial reaction proceeds in good yield in the absence of the production of any levan.
• ⁇ -Fructosyltransferase was obtained from Bacillus subtilis strain NCIB 11871.
• the enzyme was induced by sucrose during growth of the cells of shake flasks (250 ml capacity, 4 flasks) containing minimal sucrose medium (100 ml per flask). The culture was incubated until the late exponential phase, shaking at 30°C, and the contents of the four shake flasks were then combined and the growth medium separated from the cells by centrifugation (5,000 g for 15 minutes). 20-30% of the total enzyme remained associated with the cells. The resulting supernatant was brought to sixty five per cent saturation by the addition of solid ammonium sulphate and left to stand for 45 minutes atO°C.
• the dialysed enzyme was assayed before and after the addition of p-hydroxymercuribenzoate which inhibits invertase but does not affect fructosyltransferase activity.
• fructosyltransferase preparations were usually found to be free from invertase.
• the protein content of the preparations was estimated at 0.45 mg/mo by measuring their absorbance at 280 nm.
• a black pigment is often present even in the purified enzyme preparations but does not affect the activity of the preparations.
• Glucose 6-acetate 80 g dried in vacuo to constant weight
• granulated sucrose 160 g
• This solution was then extensively filtered and 28 ml of the enzyme solution added.
• the reaction mixture was then incubated at 30°C and sampled at time intervals until HPLC analysis showed that no further sucrose 6-acetate was being formed, the maximum concentration of sucrose 6-acetate reached being about 120 gl- 1 .
• the enzyme was removed by filtering the reaction mixture through a column of DEAE cellulose which adsorbs the enzyme. Alternatively it could be denatured by heating at 65°C for 1 hour. Removal of the enzyme is important as it may also catalyse the slow hydrolysis of the sucrose 6-acetate to release fructose.
• sucrose 6-acetate of at least 85% purity with an overall yield of about 50%.
• the nitial rate of the enzyme reaction was to produce 244.5 mg sucrose 6-acetate per mg of enzyme per hour.
• the yield of the enzymic step was 58% based on glucose 6-acetate consumption or 48% based on sucrose 6-acetate formation.
• Phosphorus pentachloride 140 g was added to dry dimethylformamide (250 ml) in a beaker with vigorous stirring, the temperature being maintained at 70 ⁇ 80°C stirring was continued for 1 hour and the reaction was then cooled and filtered. The crystalline product was washed with dmf (2 x 20 ml) and diethyl ether (40 ml) and dried in a desiccator to give the Vilsmeier reagent as white crystals (93 g).
• Sucrose 6-acetate syrup (41 g, actual sucrose 6-acetate conent 28 g) was dissolved in dmf and diluted to 86 ml. The solution was dried over molecular sieve and filtered.
• the reaction was concentrated to a syrup and acetylated by addition of pyridine (100 ml) and acetic anhydride (100 ml). After stirring at 50° for 2 hours, the reaction was cooled to 20°C and methanol (80 ml) was added while maintaining the temperature below 60°. The reaction was then evaporated to a syrup and extracted with hot (60°) toluene (4 x 100 ml). The toluene extracts were concentrated to a syrup and dissolved in ethyl acetate (100 ml). The ethyl acetate solution was washed with water (3 x 100 ml) and the water was back extracted with ethyl acetate (2 x 50 ml).
• the pentaacetate was dissolved in dry methanol and treated with a catalytic amount of sodium methoxide at room temperature for 5 hours. The solution was then deionised and evaporated to yield 4,1',6'-trichloro-4,1',6'-trideoxyga/actosucrose (90%).
• 6-Deoxy-D-glucose D-quinovose, 20 g
• sucrose were subjected to a reaction similar to that in Example 1, yielding a mixture of 6-deoxysucrose, d-quinovose, sucrose and glucose, total volume 140 ml.
• the 6-deoxysucrose was separated from the mixture by preparative hplc, using a Waters Prepak 500-C18 reverse-phase column) and water as eluant.
• a surprisingly large difference in retention time was observed between that of 6-deoxysucrose and those of the other components in the mixture.
• 6-Deoxysucrose (2.8 g) was dissolved in DMF (10 ml) and the solution added to a suspension of Vilsmeier reagent (15 g) in DMF (30 ml), keeping the temperature below 10°C. The mixture was stirred at room temperature for 10 min and then heated to 120°C for 2 h with stirring. The reaction was cooled to room temperature and methanol-ammonium hydroxide solution (1:1, 20 ml) added. The mixture was concentrated at 70°C and toluene (2 x 20 ml) was evaporated from the residue which was then acetylated with acetic anhydride (30 ml) in pyridine (30 ml) at 60°C for 3 h.
• Example 1 The process of Example 1 was repeated, but using glucose 6-benzoate instead of the 6-acetate in state b). A similar result was obtained and stage c) was effected as before to produce sucralose in similar yield.
• Example 1 can be modified by using an enzyme derived from the B. subtilis Marburg strain 168, strain NCIB 11872 or strain NCIB 11873 in stage b). The reaction proceeds similarly, but at a lower reaction rate.
• DEAE ion-exchange cellulose (DE 52) was washed exhaustively in 50 mM Mcllvaine Buffer pH 5.4 and then with buffered substrate (sucrose-xylose 2:1, 40% w/v), total sugars). After filtering almost to dryness on a Buchner filter, the DEAE cellulose (10 g) was mixed with 8 ml of a fructosyltransferase preparation from Bacillus subtilis as in Example 1 for fifteen minutes at 30°C with stirring. The resulting mixture of DEAE cellulose and enzyme was packed into a 10 ml jacketed column (19 x 1 cm) and maintained at 30°C with a Churchill thermocirculator. The DEAE cellulose was allowed to drain under gravity and the drainings collected.
• a substrate was pumped up the column at a flow rate of about 1.0 ml h- 1 using a Watson-Marlow pump and eluant was collected at time intervals and assayed for fructosyltransferase activity. Adsorbance at 280 nm (OD 280 ) was also measured. To assay the sample a 0.1 ml portion of the liquid sample or 0.1 g of immobilised enzyme (on DE 52) was incubated with 2 ml of substrate at 30°C for 4 hours.
• the protein concentration and activity of the depleted solution remaining after the immobilization procedure had been terminated was compared with the protein concentration and activity of the original enzyme preparation. It was found that 68.5% of the enzyme originally present in the cell extract had been immobilized together with 83% of the protein originally present.
• the immobilized enzyme had an initial activity of 80.2% of that of an equivalent quantity of free enzyme; the activities of the two preparation being 0.38 g xylsucrose/g immobilized enzyme/h and 0.865 g xylsucrose/ml enzyme extract/h respectively.
• the immobilized enzyme (10 g w/w) was run continuously, packed into a column at 30°C, for about 2 weeks without any change in the pH of the eluate or evidence of microbial contamination. A little protein and enzyme was desorbed during the first three days of operation amounting to 24% of the protein initially adsorbed and 2.3% of the enzyme activity initially adsorbed. The immobilized enzyme activity decayed with an operational half-life of 95 h and showed the usual inverse relationship between the degree of conversion of substrates into products and flow rate through the column.
• the immobilised enzyme led to some side products being formed during the reaction. A little fructose was formed, less than that produced by the original enzyme extract used for immobilization probably because the invertase activity which contaminates the extract was only partially adsorbed to the DE52.
• Several minor compounds which were eluted very late from the HPLC column with retention times of 13 and 20 min. were observed in the eluate from the immobilized enzyme although they had never been noticed during analysis of the soluble enzyme reactions. These are probably oligosaccharides formed from the usual reactants by the enzyme. It is thought that the hold up of reactant molecules by the immobilized enzyme increases their contact time with the enzyme so that the possibility of polymerization occurs.
• sucrose 6-acetate from glucose 6-acetate, 6-0-methy! sucrose from 6-0-methyl glucose, and 6-0-benzylsucrose from 6-0-benzylglucose.
• the enzyme prepared according to Example 1 (0.1 ml) was mixed with 2 ml of a 40% w/v solution of sucrose and xylose (1:1), buffered at pH 5.5 at 30°C, and the reaction was monitored.
• Xylsucrose was estimated by PHLC.
• Levan formation was estimated optically.
• the results of a comparison with various enzymes were as follows:-
• enzymes according to the invention produce at least 10 times more xylsucrose than the Marburg strain enzyme: at least 100 times more in the case of NCIB 11871 enzyme.
• the competing production of levan is much less.
• sucrose 6-acetate (5 g) in dmf (20 ml) was prepared as in Example 1 and was treated with a cooled suspension of the Vilsmeier reagent (25 g) in dmf (50 ml) was stirring, maintaining the temperature below 20°C for 30 minutes.
• the stirred mixture was then stirred at ambient temperature for 30 minutes and then heated to 110°C and stirred for a further 1.75 hours. It was then coolecd to 20°C and neutralised by addition of a 2:1 mixture of methanol and conc. (0.880) ammonia, maintaining the temperature below 40°C.
• Example 1 The mixture was then concentrated to a syrup and acetylated with acetic anhydride (100 ml) in pyridine (100 ml) at 50°C for 2 hours.
• the product was recovered as in Example 1 as the tribromogalactosucrose pentaacetate (4.2 g) identical with that in GB 2101989A.
• This was deacelylated with sodium methoxide (1 molar in methanol, at pH 9) at ambient temperature for 5 hours and then deionised with Amberlyst 15 (h + ) ion-exchange resin. The supernatant was evaporated to dryness to yield the pure tribromo sugar, identical with that in GB 2101989A.
• Xylsucrose (from Example 5) (3 g) was dissolved in dmf (6 ml) at 10°C and added with stirring to a cold suspension of the Vilsmeier reagent from Example 1 (13 g) in dmf (25 ml) maintaining the temperature below 10°C. The stirred mixture was then warmed to room temperature over 30 minutes and then to 120° and held with stirring for 3 hours. The mixture was then cooled, neutralised with 1:1 methanol/conc. (0.880 ammonia and concentrated at 70°C.
• the tetraacetate was dissolved in methanol (30 ml) and deacetylated with 1 molar sodium methoxide in methanol at pH 9, at ambient temperature.
• the compound was found to be 25x as sweet as sucrose in a 2% solution.

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• Micro-Organisms Or Cultivation Processes Thereof (AREA)
• Steroid Compounds (AREA)
• Physical Or Chemical Processes And Apparatus (AREA)

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• 1983
  • 1983-06-21 GB GB838316790A patent/GB8316790D0/en active Pending
• 1984
  • 1984-06-18 DK DK198402977A patent/DK172955B1/da not_active IP Right Cessation
  • 1984-06-20 ZA ZA844655A patent/ZA844655B/xx unknown
  • 1984-06-20 PT PT78770A patent/PT78770B/pt active IP Right Revival
  • 1984-06-20 IE IE155184A patent/IE58153B1/en not_active IP Right Cessation
  • 1984-06-20 SU SU843757905A patent/SU1630617A3/ru active
  • 1984-06-20 FI FI842513A patent/FI85160C/fi not_active IP Right Cessation
  • 1984-06-20 ES ES533607A patent/ES533607A0/es active Granted
  • 1984-06-20 CA CA000457025A patent/CA1225348A/en not_active Expired
  • 1984-06-20 AU AU29577/84A patent/AU578418B2/en not_active Expired
  • 1984-06-21 DE DE8484304206T patent/DE3481514D1/de not_active Expired - Lifetime
  • 1984-06-21 IL IL72176A patent/IL72176A/xx not_active IP Right Cessation
  • 1984-06-21 MX MX8411186U patent/MX7714E/es unknown
  • 1984-06-21 GB GB08415877A patent/GB2145080B/en not_active Expired
  • 1984-06-21 KR KR1019840003492A patent/KR850000434A/ko not_active Application Discontinuation
  • 1984-06-21 AT AT84304206T patent/ATE50774T1/de not_active IP Right Cessation
  • 1984-06-21 PH PH30866A patent/PH20732A/en unknown
  • 1984-06-21 US US06/622,853 patent/US4617269A/en not_active Expired - Lifetime
  • 1984-06-21 JP JP59128395A patent/JPH0777559B2/ja not_active Expired - Lifetime
  • 1984-06-21 NO NO842496A patent/NO162080C/no unknown
  • 1984-06-21 EP EP84304206A patent/EP0130054B1/en not_active Expired - Lifetime
  • 1984-06-21 NZ NZ208606A patent/NZ208606A/en unknown

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